A method of inhibiting the formation or deposition of wax in a mixture comprising hydrocarbons, the method comprising contacting the mixture with a composition which comprises at least one ionic liquid. The ionic liquid is preferably a polyamine salt derivative or a polypropylene glycol derivative.
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1. A method of inhibiting the formation or deposition of wax in a mixture comprising hydrocarbons, the method comprising contacting the mixture with a composition which comprises at least one ionic liquid, wherein the ionic liquid comprises a polyamine salt derivative having the formula [NH2(A-NH)nH]mpXq-, wherein A is an arylene, alkylene, or alkenylene group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m and Xq- is an anion or a polyamine salt derivative having the chemical formula [R—NH(CH2)jNH2]mpXq-, wherein R is an arylene, alkylene, or alkenylene group, j is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m and Xq- is an anion.
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The present application is a National Stage (§371) application of PCT/US2012/070136, filed Dec. 17, 2012, which claims priority from U.S. Provisional Application 61/578,334, filed Dec. 21, 2011, each of which are hereby incorporated by reference in their entirety.
The invention relates to methods and compositions for inhibiting the deposition of wax in a hydrocarbon mixture and in one embodiment to methods and compositions for inhibiting the deposition of wax during the production of oil and gas.
Crude oil produced from production wells often contains waxy components that “freeze” to form wax crystals that can adhere to the pipe or conduit and subsequently block the pipe. The wax present in crude oils primarily consists of paraffin hydrocarbons (C18-C36) known as paraffin wax and naphthenic hydrocarbons (C30-C60).
When the temperature of the crude oil is lowered, which occurs when the oil is produced from a well deep under the surface of the ocean, crystals of wax begin to form on the walls of the pipe. Wax crystals can then continue to grow in size until the whole inner wall is covered. The partial blockage of the pipe requires additional pressure to move the hydrocarbons through the pipe and could eventually result in complete blockage of the pipe.
This invention provides a method of inhibiting the formation or deposition of wax in a mixture comprising hydrocarbons, the method comprising contacting the mixture with a composition which comprises at least one ionic liquid.
This invention further provides a composition for inhibiting the formation or deposition of wax in a hydrocarbon mixture which comprises at least one ionic liquid.
This invention also provides a foam inhibited mixture comprising water, hydrocarbons, and a composition comprising at least one ionic liquid.
The present invention is directed to a method of treating hydrocarbons produced from oil and gas production wells. These hydrocarbons are prone to forming and depositing wax deposits during the production, transport and processing steps which these hydrocarbons undergo. The present invention addresses this problem by treating the hydrocarbons with a composition comprising one or more ionic liquids. The ionic liquid(s) may be combined with additional components known to those of ordinary skill in the art that are useful for treating hydrocarbons produced from hydrocarbon production wells.
Ionic liquids are generally defined as molten salts which are liquid at room temperature or by definition have a melting point of less than 100° C. They have virtually no vapor pressure and can exhibit high thermal stability. As the term ionic liquids is used in this application, it may apply to the above described molten salts or to the salts dissolved in solution, aqueous or otherwise.
An ionic liquid can be presented by the formula C+A− wherein C+ is a suitable cation and A− is a suitable anion.
A preferred embodiment of an ionic liquid is a polyamine salt derivative. The polyamine salt derivative (s) may be combined with additional components known to those of ordinary skill in the art that are useful for treating hydrocarbons produced from hydrocarbon production wells.
One embodiment of a suitable polyamine salt derivative has the general chemical formula (I):
[NH2(A-NH)nH]mpXq-
wherein A is a divalent optionally substituted hydrocarbyl group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m and Xq- is an anion.
In formula (I), A is preferably a divalent straight chain or branched hydrocarbyl group. That is to say, in formula (I), A is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group. More preferably, A is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
In the compound of formula (I), the optional substituents in the group A are preferably selected from hydroxy, halo or alkoxy groups, especially C1-4 alkoxy groups.
For example, the optionally substituted hydrocarbyl group A may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
Other examples of said optionally substituted hydrocarbyl group A in formula (I) herein include C4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenyl and phenylmethylphenyl.
In the present invention, the optionally substituted hydrocarbyl group A in formula (I) may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, amino, preferably tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl. The majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulfur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
Those skilled in the art will appreciate that functional groups such as hydroxy, halo, alkoxy, nitro and cyano in a substituted hydrocarbyl group A will displace one of the hydrogen atoms of the hydrocarbyl, whilst functional groups such as carbonyl, carboxyl, tertiary amino (—N—), oxy, sulphonyl and sulphoxyl in a substituted hydrocarbyl group will displace a —CH— or —CH2— moiety of the hydrocarbyl.
More preferably, the hydrocarbyl group A in formula (II) is unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C1-4 alkoxy.
In formula (I), n is in the range of from 1 to 100. Preferably, the lower limit of the range for n is 1, more preferably 2, even more preferably 3; preferably the upper limit of the range for n is 100, more preferably 60, more preferably 40, more preferably 20, and even more preferably 10 (i.e. n may be selected from any of the following ranges: from 1 to 100; from 2 to 100; from 3 to 100; from 1 to 60; from 2 to 60; from 3 to 60; from 1 to 40; from 2 to 40; from 3 to 40; from 1 to 20; from 2 to 20; from 3 to 20; from 1 to 10; from 2 to 10; and, from 3 to 10).
Another embodiment of a suitable polyamine salt derivative has the general chemical formula (II):
[R—NH(CH2)jNH2]mpXq-
wherein R is a divalent optionally substituted hydrocarbyl group, j is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m and Xq- is an anion.
In formula (II), R is preferably a divalent straight chain or branched hydrocarbyl group. That is to say, in formula (II), R is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group. More preferably, R is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
In the compound of formula (II), the optional substituents in the group R are preferably selected from hydroxy, halo or alkoxy groups, especially C1-4 alkoxy groups.
For example, the optionally substituted hydrocarbyl group R may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
Other examples of said optionally substituted hydrocarbyl group R in formula (II) herein include C4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenyl and phenylmethylphenyl.
In the present invention, the optionally substituted hydrocarbyl group R in formula (II) may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, amino, preferably tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl. The majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulfur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
Those skilled in the art will appreciate that functional groups such as hydroxy, halo, alkoxy, nitro and cyano in a substituted hydrocarbyl group R will displace one of the hydrogen atoms of the hydrocarbyl, whilst functional groups such as carbonyl, carboxyl, tertiary amino (—N—), oxy, sulphonyl and sulphoxyl in a substituted hydrocarbyl group will displace a —CH— or —CH2— moiety of the hydrocarbyl.
More preferably, the hydrocarbyl group R in formula (II) is unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C1-4 alkoxy.
In formula (II), j is in the range of from 1 to 100. Preferably, the lower limit of the range for j is 1, more preferably 2, even more preferably 3; preferably the upper limit of the range for j is 100, more preferably 60, more preferably 40, more preferably 20, and even more preferably 10 (i.e. j may be selected from any of the following ranges: from 1 to 100; from 2 to 100; from 3 to 100; from 1 to 60; from 2 to 60; from 3 to 60; from 1 to 40; from 2 to 40; from 3 to 40; from 1 to 20; from 2 to 20; from 3 to 20; from 1 to 10; from 2 to 10; and, from 3 to 10).
The anion Xq- of the compound of formulas (I) and (II) is not critical and can be any anion (or mixture of anions) suitable to balance the positive charge of the polyamine cation.
The anion Xq- of the compound of formulas (I) or (II) may conveniently be a sulfur-containing anion, such as an anion selected from sulfate and sulfonate anions.
However, it may be desirable to maintain a low sulfur content in the oil and gas being produced so the use of non-sulfur-containing anions in the compounds of formula (III) may be desirable depending upon the concentration of sulfur in the oil and gas and/or the desired concentration of sulfur in the oil and gas composition containing the one or more poly(hydroxycarboxylic acid) amide salt derivatives.
Therefore, the anion Xq- of the compound of formula (III) can also be any non-sulfur-containing anion (or mixture of anions) suitable to balance the positive charge of the poly(hydroxycarboxylic acid) amide cation, such as a non-sulfur-containing organic anion or a non-sulfur-containing inorganic anion.
Non-limiting examples of suitable anions are OH−, CH−, NH3−, HCO3−, HCOO−, CH3COO−, H−, BO33−, CO32−, C2H3O2−, HCO2−, C2O42−, HC2O4−, NO3−, NO2−, N3−, NH2−, O2−, O22−, BeF3−, F−, Na−, [Al(H2O)2(OH)4]−, SiO32−, SiF62−, H2PO4−, P3−, PO43−, HPO42−, Cl−, ClO3−, ClO4−, ClO−, KO−, SbOH6−, SnCl62−, [SnTe4]4−, CrO42−, Cr2O72−, MnO4−, NiCl62−, [Cu(CO3)2(OH)2]4−, AsO43−, Br−, BrO3−, IO3−, I−, CN−, OCN−, etc.
Suitable anions may also include anions derived from compounds containing a carboxylic acid group (e.g. a carboxylate anion), anions derived from compounds containing a hydroxyl group (e.g. an alkoxide, phenoxide or enolate anion), nitrogen based anions such as nitrate and nitrite, phosphorus based anions such as phosphates and phosphonates, or mixtures thereof.
Non-limiting examples of suitable anions derived from compounds containing a carboxylic acid group include acetate, oleate, salicylate anions, and mixtures thereof.
Non-limiting examples of suitable anions derived from compounds containing a hydroxyl group include phenate anions, and mixtures thereof.
In a preferred embodiment of the present invention, the anion Xq- is a non-sulfur-containing anion selected from the group consisting of OH, a phenate group, a salicylate group, an oleate group and an acetate group; more preferably the anion Xq- is OH.
Another preferred embodiment of an ionic liquid is a polypropylene glycol derivative of the formula (III):
##STR00001##
where R1 is a hydroxyl group, mono or poly organic amine, or organic alcohol; R2 and R3 are individually hydrogen or methyl groups; m and n are positive integers less than 100; p is a positive integer less than 2000; and k is a positive integer of from 1 to 4.
The ionic liquid comprising treatment fluid may be injected into a production well, into an injection well, into the hydrocarbon production system or in any other manner known to one of ordinary skill in the art. The treatment fluid may be injected at one or more locations and more than one different treatment fluid may be injected together or separately in different locations or at different times.
It is believed that the composition comprising ionic liquids is effective at reducing the wax formation and deposition because it prevents the wax from forming and dissolves any wax that has already formed.
The method of the present invention reduces or inhibits the formation or deposition of wax as shown in the following illustrative examples.
Example 1 compares the impact on wax dissolution of using an ionic liquid in combination with xylene as opposed to using xylene by itself. In this experiment, 1 gram wax deposit samples were pressed into a pill. The first wax deposit was placed into 10 ml of xylene overnight. Then the xylene was filtered out (Sample 1) and tested using high temperature simulated distillation to determine the carbon distribution of the liquid. This can be used to quantify the amount of heavier paraffins from the wax that are dissolved in the liquid. This test was repeated using 10 ml of a xylene and polyamine salt derivative mixture where the mixture was 10 wt % polyamine salt derivative. The liquid was filtered out (Sample 2) and tested using high temperature simulated distillation. An additional high temperature simulated distillation was carried out with the xylene and the polyamine salt derivative (without any wax) (Sample 3) to determine the baseline carbon distribution of that mixture.
The results are shown in
Zhang, Ying, Huo, Zhongxin, Shea, Timothy Michael, Kuijvenhoven, Cornelis Antonius Theodorus
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| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
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| Aug 18 2013 | KUIJVENHOVEN, CORNELIS ANTONIUS THEODORUS | Shell Oil Company | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 033138 | /0384 | |
| Aug 19 2013 | ZHANG, YING | Shell Oil Company | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 033138 | /0384 | |
| Jan 11 2014 | SHEA, TIMOTHY MICHAEL | Shell Oil Company | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 033138 | /0384 | |
| Feb 07 2014 | HUO, ZHONGXIN | Shell Oil Company | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 033138 | /0384 |
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